WO1999047607A1 - Resin composition - Google Patents

Resin composition Download PDF

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Publication number
WO1999047607A1
WO1999047607A1 PCT/JP1999/001323 JP9901323W WO9947607A1 WO 1999047607 A1 WO1999047607 A1 WO 1999047607A1 JP 9901323 W JP9901323 W JP 9901323W WO 9947607 A1 WO9947607 A1 WO 9947607A1
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Prior art keywords
weight
resin composition
parts
fluororesin
following
Prior art date
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PCT/JP1999/001323
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French (fr)
Japanese (ja)
Inventor
Yasuki Miura
Fukuo Kanno
Masataka Yokota
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Asahi Glass Company Ltd.
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Publication date
Application filed by Asahi Glass Company Ltd. filed Critical Asahi Glass Company Ltd.
Priority to US09/623,486 priority Critical patent/US6780944B1/en
Priority to DE69938340T priority patent/DE69938340T2/en
Priority to EP99909203A priority patent/EP1065247B1/en
Publication of WO1999047607A1 publication Critical patent/WO1999047607A1/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
    • C08L27/02Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/12Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
    • C08L27/02Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/12Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • C08L27/18Homopolymers or copolymers or tetrafluoroethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L81/00Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing sulfur with or without nitrogen, oxygen or carbon only; Compositions of polysulfones; Compositions of derivatives of such polymers
    • C08L81/02Polythioethers; Polythioether-ethers

Definitions

  • the present invention relates to a resin composition containing polyphenylene sulfide (hereinafter, referred to as PPS) and a fluororesin. More specifically, the dimensional accuracy of a molded article having a three-dimensional shape obtained by an injection molding method is significantly improved.
  • a resin composition containing polyphenylene sulfide (hereinafter, referred to as PPS) and a fluororesin. More specifically, the dimensional accuracy of a molded article having a three-dimensional shape obtained by an injection molding method is significantly improved.
  • PPS polyphenylene sulfide
  • PPS is known as a resin with excellent heat resistance, solvent resistance, electrical properties, mechanical strength, dimensional stability, flame retardancy, etc.It is used for electric and electronic equipment parts and automotive parts materials. , Chemical equipment parts materials, other functional parts materials and so on.
  • PPS has a low degree of polymerization and has the property of being compounded with fiber reinforcing agents such as glass fiber and carbon fiber and inorganic fillers, etc., and can be used as engineering plastics. This is because a phenomenon occurs in which the dimensions of the molded product differ depending on the orientation direction and it is difficult to obtain a predetermined dimensional accuracy.
  • An object of the present invention is to provide a resin composition containing PPS, a fluororesin, and a filler, from which a three-dimensional molded article having high dimensional accuracy can be obtained by injection molding.
  • the present inventors have found that the above object can be achieved by blending a specific amount of a fluororesin having a higher solidification temperature than PPS into PPS, and have accomplished the present invention.
  • the present invention relates to the following (a) and (b): (a) 50 to 99.5% by weight, (b) 0.5 to 50 in the total amount of (a) and (b).
  • a resin composition containing the resin composition in a percentage by weight.
  • the present invention provides the above resin composition containing the following (c) in a total amount of more than 0 to 250 parts by weight based on 100 parts by weight of the total of (a) and (b).
  • PPS (a) used in the present invention is substantially a repetition of the structure represented by Formula 1. It is a random copolymer or block copolymer containing at least 70 mol%, preferably at least 90 mol%, of these repeating units. If this repeating unit is less than 70 mol%, it is difficult to obtain a composition that achieves the object of the present invention.
  • the copolymer units other than the repeating unit having the structure represented by the formula 1 are present in the PPS (a) in a proportion of less than 30 mol%, preferably less than 10 mol%, and do not lower the crystallinity of the polymer. It may contain an arylene sulfide structure unit represented by the following structure within the range.
  • R represents an alkyl group, a nitro group, a phenyl group, an alkoxy group, a carboxylic acid group, or a carboxylic acid metal base.
  • PP S (a) can be obtained by various known polymerization methods.
  • a preferred method is to react sodium sulfide with p-dichlorobenzene in an amide-based solvent such as N-methylpyrrolidone or dimethylacetamide or a sulfone-based solvent such as sulfolane.
  • an amide-based solvent such as N-methylpyrrolidone or dimethylacetamide
  • a sulfone-based solvent such as sulfolane.
  • PP S (a) can be used after washing after polymerization.However, for example, it may be used after treatment with an aqueous solution containing an acid such as hydrochloric acid or acetic acid or a mixed solution of water and an organic solvent, or with a salt solution such as ammonium chloride. Even processed ones can be used.
  • the melt index of P PS (a) is measured at a cylinder temperature of 300 ° C, a load of 5 kg, an orifice diameter of 2.095 mm and a length of 8 mm, and is preferably 0.1 to 500, particularly preferably. Is 1 to 300. If the melt index is less than 0.1, the fluidity during injection molding is poor, and if it exceeds 500, the mechanical strength of the molded product is low, making it unsuitable for industrial parts.
  • the fluororesin (b) is a fluororesin having a solidification temperature (T mc ) of 237 ° C or higher when cooled at a cooling rate of 10 ° CZ after being melted in a nitrogen atmosphere of 330 ° C.
  • HFP TF EZ hexafluoropropylene copolymer
  • PFA is preferably commercially available, in which the number of carbon atoms in the alkyl group of PAVE of the polymerization component is 1 to 6 and the polymerization unit based on PAVE is 1 to 5 mol%.
  • PAVE perfluro (propyl vinyl ether), perfluor (ethyl vinyl ether), perfluoro (methyl vinyl ether) are preferable, and particularly perfluoro (propyl vinyl ether) is preferable.
  • the PF A may contain polymerized units based on two or more of these.
  • the FEP preferably has a polymerization unit of 1 to 20 mol% based on HFP and is commercially available.
  • a PAVEZHFP / TFE copolymer a polymerization component Z (PAVE and / or HFP) ZTFE copolymer other than PAVE and HFP, and the like may be used.
  • the polymerized units based on PAVE are 0 to 5 mol%
  • the polymerized units based on HFP are 0 to 20 mol%
  • the total of the polymerized units based on PAVE and HFP is 1 to 20 mol%. % Is preferred.
  • a copolymer containing 0.5 mol% of a polymerization unit based on perfluoro (propylbutyl ether) and 7.0 mol% of a polymerization unit based on HFP is used.
  • the melt index of these fluororesins (b) is not particularly limited, it is measured under the conditions of 330 ° C, 5 kg load, orifice diameter 2.095 mm and length 8 mm. It is preferable for dispersion. Melt index measurement conditions are specified in ASTM D1238.
  • fluororesins (b) can be produced by conventionally known various polymerization methods such as suspension polymerization, emulsion polymerization and solution polymerization.
  • the mixing ratio (a) / (b) of PPS (a) and fluororesin (b) in the composition of the present invention is 5050 to 99.5 / 0.5 by weight. Particularly, T O / S O S SZ 5 (weight ratio) is preferable. If the weight ratio of PPS is less than 50Z50, the fluororesin cannot clearly form islands, and if it exceeds 99.5 / 0.5, the amount of fluororesin will be small, and the effects of the present invention cannot be expected.
  • the sea portion is preferably PPS
  • the island portion is preferably formed of a fluororesin.
  • Fig. 1 shows a schematic cross-sectional view of the mold. 1 is a sprue, 2 is a runner, 3 is a pin gate, and 4 is a molded product.
  • the molded product obtained by injection molding the composition of the present invention at a cylinder temperature of 330 ° C. and a mold temperature of 150 ° C. is a molded product A shown in FIG. It has excellent dimensional accuracy, with the dimensional difference of the B part and the difference between the maximum and minimum dimensions of the B part when formed by 100 shots are about 10 times smaller than before.
  • Figure 2 is a cross-sectional view of the molded product. Indicates the dimensions and shape. The unit of the dimensions in Fig. 2 is mm, D 1 is 25.0 in diameter, D 2 is 19.0 in diameter, D 3 is 35.0 in diameter, D 4 is 24.6 in diameter, and D 5 is 22. 8, D6 is diameter 19.6, L1 is 35.0, L2 is 20.0, L3 is 5.4, L4 is 3.0, L5 is 8.0, L6 is 2.0 is there.
  • composition of the present invention contains (c) an organic reinforcing material, an inorganic reinforcing material, or a filler in addition to (a) and (b), but based on 100 parts by weight of the total of (a) and (b).
  • C) May contain up to 250 parts by weight of organic reinforcement, inorganic reinforcement or filler.
  • A) If the component exceeds 250 parts by weight, injection molding is difficult. Also, injection molding can be performed without the component (c).
  • components include organic fillers of thermosetting resin powder, fly, mica, silica, talc, alumina, kaolin, calcium sulfate, calcium carbonate, graphite, titanium oxide, zinc oxide, riichi
  • examples include inorganic fillers such as bon black, glass fiber, bonbon fiber, inorganic reinforcing material with a weak force such as potassium titanate and aluminum borate, and organic reinforcing materials such as polyimide fiber.
  • These components (c) may be used as they are, but it is preferable to use those that have been surface-treated with a silane coupling agent or the like before blending.
  • lubricants such as sodium sulfate, sodium sulfate, sodium sulfate, sodium sulfate, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite, sodium metabisulfite
  • Adjustment of the resin composition of the present invention can be performed by charging the extruder into the hopper using a number of metering feeders, or by premixing using a tumbler, V mixer, hensile mixer, etc.
  • a method of selecting a screw with a bidding function with a kneading machine, melting and kneading to make a pellet is used.
  • the sample was heated from normal temperature to 330 ° C at a rate of 10 ° C / minute under a nitrogen atmosphere, and maintained at 330 ° C for 5 minutes. The temperature was lowered from 10 ° C. to 100 ° C. in 10 ° C.Z for measurement.
  • PTFE Asahi Glass Co., Ltd., full-on PTFE L-150 J (no coagulation temperature).
  • PF A manufactured by Asahi Glass Co., Ltd., Aflon PF A P-61 (with a solidification temperature of 271).
  • FEP Aflon FEP (solidification temperature 241) manufactured by Asahi Glass Co., Ltd.
  • ETFE Asahi Glass Co., Ltd., Aflon COPC88AX (coagulation temperature 230 ° C).
  • Low melting point ETF E hereinafter referred to as LM-ETFE
  • Aflon LM 740 solidification temperature 206 ° C, manufactured by Asahi Glass Co., Ltd.
  • PVdF NEOFLON VP 800 (coagulation temperature: 150 ° C), manufactured by Daikin.
  • Glass fiber 03MAFT 562, manufactured by Asahi Fiber One Glass Co., Ltd.
  • No surface treatment was performed with a silane coupling agent before blending glass fiber, spherical silica, or calcium carbonate.
  • Table 1 shows the PPS and filler in the hopper of the first feeder and the fluororesin in the hopper of the second feeder of the same-direction twin-screw extruder with a kneading section having two kneading points.
  • a cylinder temperature of 320 ° C a screw rotation speed of lOO rpm, the raw materials are kneaded while sucking with a vacuum pump from the vent, and the discharged strand is gradually cooled and then 3 mm long with a beretizer.
  • the cylinder temperature of a molding machine of 30 tons for electric type mold clamping, which was cut into pieces to prepare a composition was set to 330.
  • the outer diameter of points A and B in Fig. 2 was measured using a laser scan micrometer (manufactured by Mitutoyo Corporation) for the obtained molded article.
  • the dimensional difference between parts A and B (wm) (hereinafter referred to as AZB dimensional difference) and the difference between the maximum and minimum dimensions of part B of a 100 shot molded product (wm) (hereinafter referred to as B dimensional difference) are shown. Shown in 1. [table 1 ]
  • the resin composition of the present invention has extremely high dimensional accuracy of a molded article having a three-dimensional shape obtained by injection molding the resin composition, and is useful for structural materials and various parts in the fields of automobiles, home appliances, and electronics.

Abstract

A resin composition which comprises: 50 to 99.5 parts by weight of poly(phenylene sulfide); 0.5 to 50 parts by weight of a fluororesin which, when melted in a 330 °C nitrogen atmosphere and then cooled at a rate of 10 °C/min, has a solidification temperature of 237 °C or higher; and a filler and other optional ingredients in an amount of 0 to 250 parts by weight per 100 parts by weight of the sum of the polymers.

Description

明細書  Specification
樹脂組成物  Resin composition
技術分野 Technical field
本発明は、 ポリフヱニレンスルフィ ド (以下、 PP Sという) とフッ素樹脂を 含有する樹脂組成物に関し、 詳しくは射出成形法によって得られる立体形状を有 する成形品の寸法精度が著しく改善される樹脂組成物に関する。  The present invention relates to a resin composition containing polyphenylene sulfide (hereinafter, referred to as PPS) and a fluororesin. More specifically, the dimensional accuracy of a molded article having a three-dimensional shape obtained by an injection molding method is significantly improved. A resin composition.
背景技術 Background art
P P Sは、 耐熱性、 耐溶剤性、 電気特性、 機械的強度、 寸法安定性、 難燃性等 が優れた樹脂として知られており、 その用途には電気 ·電子機器部品材料や自動 車部品材料、 化学機器部品材料、 その他の機能部品材料などがある。  PPS is known as a resin with excellent heat resistance, solvent resistance, electrical properties, mechanical strength, dimensional stability, flame retardancy, etc.It is used for electric and electronic equipment parts and automotive parts materials. , Chemical equipment parts materials, other functional parts materials and so on.
これらの大部分の用途において、 射出成形法によって成形された部品が用いら れている。 しかし、 要求される特性は細分化され、 例えば従来金属を切削加工な どで加工していた部品のうちには特に高い寸法精度が要求されるものがあるが、 Most of these uses injection molded parts. However, the required characteristics are subdivided.For example, some parts that have conventionally been processed by metal, such as cutting, require particularly high dimensional accuracy.
P P Sによる代替が困難であった。 Substitution by PPS was difficult.
その理由は、 PPSは重合度が低いためガラス繊維、 炭素繊維などの繊維補強 剤や無機充填剤などと複合化してエンジニアリングブラスチックとして通用する 特性を有するが、 射出成形した場合に繊維補強材の配向方向によって成形品の寸 法が異なる現象が生じ所定の寸法精度を得がたいためである。  The reason is that PPS has a low degree of polymerization and has the property of being compounded with fiber reinforcing agents such as glass fiber and carbon fiber and inorganic fillers, etc., and can be used as engineering plastics. This is because a phenomenon occurs in which the dimensions of the molded product differ depending on the orientation direction and it is difficult to obtain a predetermined dimensional accuracy.
また、 配向方向性の問題が生じない無機充填材、 例えばガラスビース、 酸化亜 鉛、 炭酸カルシウムなどを PP Sに配合した場合、 射出成形時の充填材の配向の 問題は解消されるが、 成形ショッ ト間のバラツキが大きく、 要求される寸法精度 を満足させえない。  In addition, when inorganic fillers that do not cause orientation direction problems, such as glass beads, zinc oxide, and calcium carbonate, are blended into PPS, the problem of filler orientation during injection molding is solved, but molding The variation between shots is large, and the required dimensional accuracy cannot be satisfied.
例えば、 立体形状を有する成形品の高い寸法精度を得るため、 PP Sと特定の シラン処理されたシリカ粉末を含む組成物を光ファイバ用コネクタフヱルールに 成形する提案 (特開平 6— 299072) や、 テトラフルォロエチレン (以下、 TF Eという) / /ペルフルォロ (アルキルビュルエーテル) (以下、 PAVEと いう) 共重合体 (以下、 PFAという) に対して PPSを 0. 5〜5重量%配合 した組成物を回転成形法によりライニングする提案 (特開平 5— 1 12690) があるが、 本発明の組成物とは組成割合が異なる。 For example, in order to obtain high dimensional accuracy of a molded article having a three-dimensional shape, a proposal for molding a composition containing PPS and a specific silane-treated silica powder into an optical fiber connector ferrule (Japanese Patent Laid-Open No. 6-2999072) and, tetrafurfuryl O b ethylene (hereinafter, TF referred E) / / Perufuruoro (alkyl Bulle ether) (hereinafter referred to as PAVE) copolymer (hereinafter referred to as PFA) PPS a 0.5 to 5% by weight with respect to Proposal for lining the blended composition by rotational molding (Japanese Patent Laid-Open No. 5-112690) However, the composition ratio is different from the composition of the present invention.
特定量の P P s、 フッ素樹脂、 球状充填材、 繊維充填材からなる,組成物により シリンダビス卜ンをィンサート成形して油中寸法安定性、 耐摩耗性が向上した成 形品を得る提案 (特開平 3— 74681 ) 、 P PS、 ポリフッ化ビユリデン (以 下、 PV d Fという) 、 及び TFEの単独重合体又は共重合体を有する組成物か ら成形品を得る提案 (特開平 5— 29520) 、 P P Sと融点が 320°C以下の フッ素樹脂とアミノアルコキシシランとを含む組成物において、 P P Sとフッ素 樹脂の相互の分散性を改善し、 その成形品の機械的強度を改善する提案 (特開平 8 - 53592) もあるが、 高い寸法精度の成形品が得られるかについては記載 されてない。  A proposal to obtain molded products with improved dimensional stability in oil and abrasion resistance by insert molding cylinder piston with a composition consisting of a specific amount of PP s, fluororesin, spherical filler, and fiber filler. JP-A-3-74681), a proposal to obtain a molded article from a composition having a homopolymer or copolymer of PPS, polyvinylidene fluoride (hereinafter referred to as PVdF), and TFE (Japanese Patent Laid-Open No. 5-29520) ), In a composition containing PPS, a fluororesin having a melting point of 320 ° C or less, and aminoalkoxysilane, a proposal to improve the mutual dispersibility of the PPS and the fluororesin, and to improve the mechanical strength of the molded product. Kaihei 8-53592), but it does not describe whether molded products with high dimensional accuracy can be obtained.
発明の開示 Disclosure of the invention
本発明の目的は、 射出成形により高い寸法精度を有する立体形状の成形品が得 られる、 P P S、 フッ素樹脂、 さらには充填材などを含む樹脂組成物を提供する ことにある。  An object of the present invention is to provide a resin composition containing PPS, a fluororesin, and a filler, from which a three-dimensional molded article having high dimensional accuracy can be obtained by injection molding.
本発明者は鋭意検討した結果、 P P Sよりも高い凝固温度を有するフッ素樹脂 の特定量を P P sに配合することにより、 上記目的を達成できることを見出し、 本発明に至った。  As a result of diligent studies, the present inventors have found that the above object can be achieved by blending a specific amount of a fluororesin having a higher solidification temperature than PPS into PPS, and have accomplished the present invention.
すなわち、 本発明は、 下記 (a) と下記 (b) とを、 (a) と (b) との合量 中に (a) 50〜99. 5重量%、 (b) 0. 5〜50重量%の割合で含有する 樹脂組成物を提供する。  That is, the present invention relates to the following (a) and (b): (a) 50 to 99.5% by weight, (b) 0.5 to 50 in the total amount of (a) and (b). Provided is a resin composition containing the resin composition in a percentage by weight.
さらに、 下記 (c) を合量で、 (a) と (b) との合量 1 00重量部に対して 0重量部超 250重量部以下の割合で含有する上記樹脂組成物を提供する。  Further, the present invention provides the above resin composition containing the following (c) in a total amount of more than 0 to 250 parts by weight based on 100 parts by weight of the total of (a) and (b).
(a) ポリフエ二レンスルフィ ド。  (a) Polyphenylene sulfide.
(b) 330°C窒素雰囲気下で溶融後 1 0°CZ分の冷却速度で冷却した場合の 凝固温度 (Tmc) が 237°C以上であるフッ素樹脂。 (b) A fluororesin having a solidification temperature (T mc ) of 237 ° C or higher when cooled at a cooling rate of 10 ° CZ after being melted in a nitrogen atmosphere at 330 ° C.
(c) 有機強化材、 無機強化材及び充填材からなる群から選ばれる 1種以上。 発明を実施するための最良の形態  (c) at least one selected from the group consisting of organic reinforcements, inorganic reinforcements and fillers. BEST MODE FOR CARRYING OUT THE INVENTION
本発明で用いられる P P S (a) は、 実質的に式 1で表される構造の繰り返し 単位からなる重合体であり、 この繰り返し単位を 70モル%以上、 好ましくは 9 0モル%以上含むランダム共重合体又はプロック共重合体である。 この繰り返し 単位が 70モル%未満では本発明の目的を達する組成物は得にくい。 PPS (a) used in the present invention is substantially a repetition of the structure represented by Formula 1. It is a random copolymer or block copolymer containing at least 70 mol%, preferably at least 90 mol%, of these repeating units. If this repeating unit is less than 70 mol%, it is difficult to obtain a composition that achieves the object of the present invention.
£<2> - S 式 ( 1£ <2>-S expression (1
Figure imgf000005_0001
式 1で表される構造の繰り返し単位以外の共重合単位は、 P P S (a) 中に 3 0モル%未満、 好ましくは 10モル%未満の割合で存在し、 重合体の結晶化度を 低下させない範囲で下記の構造で表されるァリーレンスルフィ ド構造の単位を含 有してもよい。
Figure imgf000005_0001
The copolymer units other than the repeating unit having the structure represented by the formula 1 are present in the PPS (a) in a proportion of less than 30 mol%, preferably less than 10 mol%, and do not lower the crystallinity of the polymer. It may contain an arylene sulfide structure unit represented by the following structure within the range.
Figure imgf000005_0002
― \
Figure imgf000005_0002
― \
S 0 o -s-
Figure imgf000005_0003
S 0 o -s-
Figure imgf000005_0003
[輪 +  [Ring +
(Rはアルキル基、 ニトロ基、 フヱニル基、 アルコキシ基、 カルボン酸基、 又 はカルボン酸金属塩基を示す。 ) (R represents an alkyl group, a nitro group, a phenyl group, an alkoxy group, a carboxylic acid group, or a carboxylic acid metal base.)
PP S (a) は、 公知の種々の重合方法により得られる。 硫化ナトリウムと p ージクロルベンゼンを N—メチルピロリ ドン、 ジメチルァセ卜アミ ドなどのアミ ド系溶媒ゃスルホランなどのスルホン系溶媒中で反応させる方法が好適である。 この際に重合度を調節するために酢酸ナトリウム、 酢酸リチウムなどのアル力リ 金属カルボン酸塩を添加することは好ましい。 PP S (a) can be obtained by various known polymerization methods. A preferred method is to react sodium sulfide with p-dichlorobenzene in an amide-based solvent such as N-methylpyrrolidone or dimethylacetamide or a sulfone-based solvent such as sulfolane. At this time, to adjust the degree of polymerization, sodium hydroxide, lithium acetate, etc. It is preferred to add a metal carboxylate.
PP S (a) は重合終了後に洗浄したものを使用できるが、 さらに、 例えば塩 酸、 酢酸などの酸を含む水溶液又は水 -有機溶剤混合液で処理したものや、 塩化 アンモニゥムなどの塩溶液で処理したものでも使用できる。 P PS (a) のメル 卜インデックスは、 シリンダ温度 300°C、 5 k g荷重、 オリフィスの径 2. 0 95mm, 長さ 8 mmの条件で測定し、 好ましくは 0. 1〜500、 特に好まし くは 1〜300である。 メルトインデックスが 0. 1未満では射出成形時の流動 性が劣り、 500超では成形品の機械的強度が低く、 工業部品に適さない。  PP S (a) can be used after washing after polymerization.However, for example, it may be used after treatment with an aqueous solution containing an acid such as hydrochloric acid or acetic acid or a mixed solution of water and an organic solvent, or with a salt solution such as ammonium chloride. Even processed ones can be used. The melt index of P PS (a) is measured at a cylinder temperature of 300 ° C, a load of 5 kg, an orifice diameter of 2.095 mm and a length of 8 mm, and is preferably 0.1 to 500, particularly preferably. Is 1 to 300. If the melt index is less than 0.1, the fluidity during injection molding is poor, and if it exceeds 500, the mechanical strength of the molded product is low, making it unsuitable for industrial parts.
フッ素樹脂 ( b ) は、 330 °C窒素雰囲気下で溶融後 1 0 °CZ分の冷却速度で 冷却した場合の凝固温度 (Tmc) が 237°C以上であるフッ素樹脂である。 The fluororesin (b) is a fluororesin having a solidification temperature (T mc ) of 237 ° C or higher when cooled at a cooling rate of 10 ° CZ after being melted in a nitrogen atmosphere of 330 ° C.
具体的には、 P FA、 T F EZへキサフルォロプロピレン (以下、 HFPとい う) 共重合体 (以下、 FEPという) が挙げられる。  Specifically, PFA, TF EZ hexafluoropropylene (hereinafter, referred to as HFP) copolymer (hereinafter, referred to as FEP) may be mentioned.
P FAは、 その重合成分の PAVEのアルキル基の炭素数が 1〜6であり、 P A V Eに基づく重合単位が 1〜5モル%であるものが好ましく、 市販されている 。 PAVEとして、 ペルフル才ロ (プロピルビニルエーテル) 、 ペルフルォロ ( ェチルビ二ルェ一テル) 、 ペルフルォロ (メチルビニルエーテル) が好ましく、 特にペルフルォロ (プロピルビュルエーテル) が好ましい。 P F Aはこれらの 2 種以上に基づく重合単位を含んでいてもよい。  PFA is preferably commercially available, in which the number of carbon atoms in the alkyl group of PAVE of the polymerization component is 1 to 6 and the polymerization unit based on PAVE is 1 to 5 mol%. As the PAVE, perfluro (propyl vinyl ether), perfluor (ethyl vinyl ether), perfluoro (methyl vinyl ether) are preferable, and particularly perfluoro (propyl vinyl ether) is preferable. The PF A may contain polymerized units based on two or more of these.
F E Pは、 H F Pに基づく重合単位が 1〜20モル%であるものが好ましく、 市販されている。  The FEP preferably has a polymerization unit of 1 to 20 mol% based on HFP and is commercially available.
また、 P FA、 FEP以外のフッ素樹脂 (b) として、 PAVEZHFP/T F E共重合体、 PAVEと HFP以外の重合成分 Z ( P A V E及び/又は H F P ) ZTFE共重合体などを用いてもよい。 これらの共重合体中の PAVEに基づ く重合単位が 0〜5モル%、 H F Pに基づく重合単位が 0〜20モル%であり、 PAVEと HF Pに基づく重合単位の合計が 1 ~ 20モル%のものが好適である 。 具体的には、 例えば、 ペルフルォロ (プロピルビュルエーテル) に基づく重合 単位を 0. 5モル%、 H F Pに基づく重合単位を 7. 0モル%含む共重合体が用 いられる。 これらのフッ素樹脂 (b) のメルトインデックスは特に限定されないが、 33 0°C、 5 k g荷重、 オリフィスの径 2. 095mm, 長さ 8 mmの条件で測定し 0. 1以上のものが容易に分散するため好ましい。 メル卜インデックスの測定条 件は ASTM D 1238に規定されたいる。 Further, as the fluororesin (b) other than PFA and FEP, a PAVEZHFP / TFE copolymer, a polymerization component Z (PAVE and / or HFP) ZTFE copolymer other than PAVE and HFP, and the like may be used. In these copolymers, the polymerized units based on PAVE are 0 to 5 mol%, the polymerized units based on HFP are 0 to 20 mol%, and the total of the polymerized units based on PAVE and HFP is 1 to 20 mol%. % Is preferred. Specifically, for example, a copolymer containing 0.5 mol% of a polymerization unit based on perfluoro (propylbutyl ether) and 7.0 mol% of a polymerization unit based on HFP is used. Although the melt index of these fluororesins (b) is not particularly limited, it is measured under the conditions of 330 ° C, 5 kg load, orifice diameter 2.095 mm and length 8 mm. It is preferable for dispersion. Melt index measurement conditions are specified in ASTM D1238.
なお、 これらのフッ素樹脂 (b) は懸濁重合、 乳化重合、 溶液重合などの従来 公知の各種重合方法により製造できる。  These fluororesins (b) can be produced by conventionally known various polymerization methods such as suspension polymerization, emulsion polymerization and solution polymerization.
本発明の組成物の PPS (a) とフッ素樹脂 (b) の配合割合 (a) / (b) は、 重量比で 50 50〜99. 5/0. 5である。 特に、 T O/S O S SZ 5 (重量比) が好ましい。 P P Sの重量比が 50Z50未満では、 フッ素樹脂が 明確に島を形成できなくなり、 99. 5/0. 5超ではフッ樹脂の量が少なくな り、 本発明の効果が期待できない。 組成物のマトリックスにおいて海の部分が P P Sであり、 島の部分がフッ素樹脂で形成することが好ましい。  The mixing ratio (a) / (b) of PPS (a) and fluororesin (b) in the composition of the present invention is 5050 to 99.5 / 0.5 by weight. Particularly, T O / S O S SZ 5 (weight ratio) is preferable. If the weight ratio of PPS is less than 50Z50, the fluororesin cannot clearly form islands, and if it exceeds 99.5 / 0.5, the amount of fluororesin will be small, and the effects of the present invention cannot be expected. In the matrix of the composition, the sea portion is preferably PPS, and the island portion is preferably formed of a fluororesin.
本発明の組成物から得られる成形品が高い寸法精度を有するという効果は、 P P S (a) が凝固する前にフッ素樹脂が凝固する場合に生じやすい。 この効果の 発生機構について、 ( 1 ) PPS (a) にフッ素樹脂 (b) を配合したことによ り溶融した組成物が金型のゲート通過時に射出圧力の圧力損失が低減する。 この 理由として、 フッ素樹脂が内部潤滑剤として作用するためと考えられる。 その結 果金型内の組成物に射出圧力が有効に伝わる。 図 1に金型の断面図の概略を示す 。 1はスプル、 2はランナー、 3はピンゲート、 4は成形品である。  The effect that the molded article obtained from the composition of the present invention has high dimensional accuracy is likely to occur when the fluororesin solidifies before PPS (a) solidifies. Regarding the mechanism by which this effect occurs, (1) The pressure loss of the injection pressure is reduced when the molten composition passes through the gate of the mold by blending the fluororesin (b) with the PPS (a). This is probably because the fluororesin acts as an internal lubricant. As a result, the injection pressure is effectively transmitted to the composition in the mold. Fig. 1 shows a schematic cross-sectional view of the mold. 1 is a sprue, 2 is a runner, 3 is a pin gate, and 4 is a molded product.
(2) ゲートシールする前、 すなわち保圧力が金型内の組成物に有効に作用す る状態で、 フッ素樹脂 (b) が固化し、 ゲートシールした後に P P S (a) が固 化する。 この 2段階の固化工程を経て、 ゲートシールした後の体積収縮量が低減 する。 以上の作用により、 金型転写性及び成形ショッ ト間のバラツキが抑制され 、 本発明の効果が発生したと推測される。  (2) Fluororesin (b) solidifies before the gate seal, that is, with the holding pressure effectively acting on the composition in the mold, and PPS (a) solidifies after the gate seal. Through these two-stage solidification processes, the volume shrinkage after gate sealing is reduced. It is presumed that the effects of the present invention have been produced by the above-described effects, whereby the mold transferability and the variation between molding shots were suppressed.
具体的には、 本発明の組成物を実施例で示すようにシリンダ温度 330°C、 金 型温度 1 50°Cで射出成形して得られる成形品は、 図 2に示す成形品 A部、 B部 の寸法差、 1 00ショッ ト成形したときの B部の最大寸法と最小寸法の差が従来 よりも約 1ノ1 0となる優れた寸法精度を有する。 図 2は成形品の断面図であり 寸法形状を示す。 図 2中の寸法の単位は mmであり、 D 1は直径 25. 0、 D 2 は直径 19. 0、 D 3は直径 35. 0、 D 4は直径 24. 6、 D 5は直径 22. 8、 D 6は直径 19. 6、 L 1は 35. 0、 L 2は 20. 0、 L3は 5. 4、 L 4は 3. 0、 L 5は 8. 0、 L6は 2. 0である。 Specifically, as shown in the examples, the molded product obtained by injection molding the composition of the present invention at a cylinder temperature of 330 ° C. and a mold temperature of 150 ° C. is a molded product A shown in FIG. It has excellent dimensional accuracy, with the dimensional difference of the B part and the difference between the maximum and minimum dimensions of the B part when formed by 100 shots are about 10 times smaller than before. Figure 2 is a cross-sectional view of the molded product. Indicates the dimensions and shape. The unit of the dimensions in Fig. 2 is mm, D 1 is 25.0 in diameter, D 2 is 19.0 in diameter, D 3 is 35.0 in diameter, D 4 is 24.6 in diameter, and D 5 is 22. 8, D6 is diameter 19.6, L1 is 35.0, L2 is 20.0, L3 is 5.4, L4 is 3.0, L5 is 8.0, L6 is 2.0 is there.
また、 本発明の組成物は (a) と (b) 以外に (c) 有機強化材、 無機強化材 又は充填材を含有するが、 (a) と (b) の合計 100重量部に対して (c) 有 機強化材、 無機強化材又は充填材を 250重量部以下を含有してもよい。 (a) 成分が 250重量部超では射出成形ができにくレ、。 また、 (c) 成分を含まなく ても射出成形ができる。  The composition of the present invention contains (c) an organic reinforcing material, an inorganic reinforcing material, or a filler in addition to (a) and (b), but based on 100 parts by weight of the total of (a) and (b). (C) May contain up to 250 parts by weight of organic reinforcement, inorganic reinforcement or filler. (A) If the component exceeds 250 parts by weight, injection molding is difficult. Also, injection molding can be performed without the component (c).
(c) 成分の具体例として、 熱硬化性樹脂粉末の有機充填材、 フ ライ ト、 マ イカ、 シリカ、 タルク、 アルミナ、 カオリン、 硫酸カルシウム、 炭酸カルシウム 、 黒鉛、 酸化チタン、 酸化亜鉛、 力一ボンブラックなどの無機充填材、 ガラス繊 維、 力一ボン繊維、 チタン酸カリウムやホウ酸アルミニウムなどゥイス力の無機 強化材、 ポリイミ ド繊維などの有機強化材が挙げられる。 これらの (c) 成分は そのまま用いてもよいが、 配合前にシランカップリング剤などで表面処理したも のを用いることが好ましい。  (c) Specific examples of the components include organic fillers of thermosetting resin powder, fly, mica, silica, talc, alumina, kaolin, calcium sulfate, calcium carbonate, graphite, titanium oxide, zinc oxide, riichi Examples include inorganic fillers such as bon black, glass fiber, bonbon fiber, inorganic reinforcing material with a weak force such as potassium titanate and aluminum borate, and organic reinforcing materials such as polyimide fiber. These components (c) may be used as they are, but it is preferable to use those that have been surface-treated with a silane coupling agent or the like before blending.
その他必要に応じて滑剤、 安定剤、 顔料なども添加してもよい。  In addition, lubricants, stabilizers, pigments and the like may be added as necessary.
本発明の樹脂組成物の調整は、 多数の計量フィーダを使って押出機のホッパー に投入するか、 又はタンブラや Vミキサ、 ヘンシヱルミキサなどで予備混合のう え、 同方向又は異方向の二軸押出混練機で二一ディング機能付きのスクリユーを 選択し、 溶融混練してペレツ 卜化する方法が用いられる。  Adjustment of the resin composition of the present invention can be performed by charging the extruder into the hopper using a number of metering feeders, or by premixing using a tumbler, V mixer, hensile mixer, etc. A method of selecting a screw with a bidding function with a kneading machine, melting and kneading to make a pellet is used.
以下に実施例 (例 1、 2、 8、 9) 、 比較例 (例 3〜7、 10-1 3) を挙げ て、 本発明をより具体的に説明するが、 本発明はこれらに限定されない。  Hereinafter, the present invention will be described more specifically with reference to Examples (Examples 1, 2, 8, and 9) and Comparative Examples (Examples 3 to 7 and 10-13), but the present invention is not limited thereto. .
[凝固温度の測定]  [Measurement of solidification temperature]
熱分析システム S S C 5200 (セイコー電子工業社製) を用い、 試料を窒素 雰囲気下で常温から 330°Cまで 1 0°C/分で昇温し 330°Cで 5分保持した後 、 33 (TCから 1 00 °Cまで 10 °CZ分で降温して測定した。  Using a thermal analysis system SSC 5200 (manufactured by Seiko Instruments Inc.), the sample was heated from normal temperature to 330 ° C at a rate of 10 ° C / minute under a nitrogen atmosphere, and maintained at 330 ° C for 5 minutes. The temperature was lowered from 10 ° C. to 100 ° C. in 10 ° C.Z for measurement.
[使用原材料】 P P S ;東レ社製、 M - 2 100 (凝固温度 237°C) 。 [Raw materials used] PPS: Toray Co., Ltd., M-2100 (solidification temperature 237 ° C).
PTFE ;旭硝子社製、 フルオン PTFE L— 1 50 J (凝固温度なし) 。 P F A ;旭硝子社製、 ァフロン P F A P- 61 (凝固温度 271で) 。 F EP ;旭硝子社製、 ァフロン FEP (凝固温度 241 ) 。  PTFE; Asahi Glass Co., Ltd., full-on PTFE L-150 J (no coagulation temperature). PF A: manufactured by Asahi Glass Co., Ltd., Aflon PF A P-61 (with a solidification temperature of 271). FEP: Aflon FEP (solidification temperature 241) manufactured by Asahi Glass Co., Ltd.
ETFE ;旭硝子社製、 ァフロン CO P C 88 AX (凝固温度 230°C) 。 低融点 ETF E (以下、 LM— ETFEという) ;旭硝子社製、 ァフロン LM 740 (凝固温度 206°C) 。  ETFE; Asahi Glass Co., Ltd., Aflon COPC88AX (coagulation temperature 230 ° C). Low melting point ETF E (hereinafter referred to as LM-ETFE); Aflon LM 740 (solidification temperature 206 ° C), manufactured by Asahi Glass Co., Ltd.
PVdF ; ダイキン社製、 ネオフロン VP 800 (凝固温度 1 50°C) 。 ガラス繊維;旭ファイバ一グラス社製、 03MAFT 562。  PVdF: NEOFLON VP 800 (coagulation temperature: 150 ° C), manufactured by Daikin. Glass fiber: 03MAFT 562, manufactured by Asahi Fiber One Glass Co., Ltd.
球状シリ力 ;電気化学工業社製、 F B— 35。  Spherical force: FB-35, manufactured by Denki Kagaku Kogyo.
炭酸カルシウム ; 日東粉化工業社製、 NS 200。  Calcium carbonate: NS 200 manufactured by Nitto Powder Chemical Industry Co., Ltd.
なお、 ガラス繊維、 球状シリカ、 炭酸カルシウムを配合前にシランカップリン グ剤などで表面処理を行っていない。  No surface treatment was performed with a silane coupling agent before blending glass fiber, spherical silica, or calcium carbonate.
[例 1〜6]  [Examples 1-6]
2力所のニーディング部を有するスクリユーがセッ 卜された同方向二軸押出混 練機の第一フィ一ダのホッパに P P Sと充填材を、 第二フィーダのホッパにフッ 素樹脂を表 1に示す重量比で投入し、 シリンダ温度 320°C、 スクリュー回転数 l O O r pmとし、 ベントから真空ポンプで吸引しながら原材料を混練し、 吐出 されたストランドを徐冷後べレタイザで 3 m m長さに切断して組成物を作成した 電動タイプの型締め 30トンの成形機のシリンダ温度を 330 に設定した。 図 1に示す 3点のピンボイントゲ一卜で注入され、 つば付き円筒スリーブ形状が 彫り込まれた金型を熱媒にて 1 50°Cに加温し、 作成した組成物を射出速度 80 mm/秒、 S O O k gZcm2 の条件で射出成形して成形品を得た。 Table 1 shows the PPS and filler in the hopper of the first feeder and the fluororesin in the hopper of the second feeder of the same-direction twin-screw extruder with a kneading section having two kneading points. At a cylinder temperature of 320 ° C, a screw rotation speed of lOO rpm, the raw materials are kneaded while sucking with a vacuum pump from the vent, and the discharged strand is gradually cooled and then 3 mm long with a beretizer. The cylinder temperature of a molding machine of 30 tons for electric type mold clamping, which was cut into pieces to prepare a composition, was set to 330. The mold injected with the three pin-point gauging shown in Fig. 1 and engraved with a cylindrical sleeve with a flange was heated to 150 ° C with a heating medium, and the created composition was injected at an injection speed of 80 mm / sec. to obtain a molded article by injection molding under the conditions of SOO k gZcm 2.
得られた成形品について、 レーザースキャンマイクロメータ (ミツトヨ社製) で、 図 2の A、 Bの箇所の外径を測定した。 A部、 B部の寸法差 (wm) (以下 、 AZB寸法差という) 、 1 00ショッ ト成形品の B部の最大寸法と最小寸法の 差 (wm) (以下、 B寸法差という) を表 1に示す。 [表 1 ] The outer diameter of points A and B in Fig. 2 was measured using a laser scan micrometer (manufactured by Mitutoyo Corporation) for the obtained molded article. The dimensional difference between parts A and B (wm) (hereinafter referred to as AZB dimensional difference) and the difference between the maximum and minimum dimensions of part B of a 100 shot molded product (wm) (hereinafter referred to as B dimensional difference) are shown. Shown in 1. [table 1 ]
Figure imgf000010_0001
Figure imgf000010_0001
[例 7〜1 2 ] [Examples 7 to 12]
表 2に示す重量比で、 例 1〜 6で用いた混練機の第一フィ一ダのホッパに P P Sと充填材を、 第二フィーダのホツバにフッ素樹脂を投入し、 さらにガラス繊維 をサイ ドフィ一ド方式で押出機へ投入して、 例 1〜6と同様に混練し組成物を作 成し、 その後成形して成形品を得た。 その成形品について測定した外径の結果を 表 2に示す。 [表 2] 組成 例 8 例 9 例 10 例 11 例 12 例 13 At the weight ratio shown in Table 2, PPS and filler were put into the hopper of the first feeder of the kneading machine used in Examples 1 to 6, fluororesin was put into the hopper of the second feeder, and the glass fiber was put into the side feeder. The mixture was charged into an extruder in a one-way system and kneaded in the same manner as in Examples 1 to 6 to form a composition, and then molded to obtain a molded product. Table 2 shows the results of the measured outer diameter of the molded product. [Table 2] Composition Example 8 Example 9 Example 10 Example 11 Example 12 Example 13
P P S 90 90 90 90 90 90 フッ素樹脂 P T F E 10 P P S 90 90 90 90 90 90 Fluororesin P T F E 10
P F A 10  P F A 10
F E P 10  F E P 10
E T F E 10 LM- ET F E 10 P V d F 10 充填剤 炭酸カルシウム 40 40 40 40 40 40 ガラス繊維 60 60 60 60 60 60  E T F E 10 LM- ET F E 10 P V d F 10 Filler Calcium carbonate 40 40 40 40 40 40 Glass fiber 60 60 60 60 60 60
AZB寸法差 10 82 43 50 70 B寸法差 8 68 25 19 33 AZB dimension difference 10 82 43 50 70 B dimension difference 8 68 25 19 33
産業上の利用可能性 Industrial applicability
本発明の樹脂組成物は、 これを射出成形して得られる立体形状を有する成形品 の寸法精度がきわめて高く、 自動車や家電 ·電子分野の構造材料や各種部品の用 途に有用である。  INDUSTRIAL APPLICABILITY The resin composition of the present invention has extremely high dimensional accuracy of a molded article having a three-dimensional shape obtained by injection molding the resin composition, and is useful for structural materials and various parts in the fields of automobiles, home appliances, and electronics.

Claims

請求の範囲 The scope of the claims
1. 下記 (a) と下記 (b) とを、 (a) と (b) との合量中に (a) 50〜9 9. 5重量%、 (b) 0. 5〜 50重量%の割合で含有する樹脂組成物。  1. The following (a) and (b) are combined with (a) 50 to 9.5% by weight and (b) 0.5 to 50% by weight in the combined amount of (a) and (b). Resin composition containing in proportion.
(a) ポリフエ二レンスルフィ ド。  (a) Polyphenylene sulfide.
(b) 330°C窒素雰囲気下で溶融後 1 0 CZ分の冷却速度で冷却した場合の 凝固温度 (Tmc) が 237 C以上であるフッ素樹脂。 (b) A fluororesin having a solidification temperature (T mc ) of 237 C or more when cooled at a cooling rate of 10 CZ after being melted in a nitrogen atmosphere at 330 ° C.
2. さらに、 下記 (c) を合量で、 (a) と (b) との合量 1 00重量部に対し て 0重量部超 250重量部以下の割合で含有する請求項 1記載の樹脂組成物。  2. The resin according to claim 1, further comprising the following (c) in a total amount of more than 0 to 250 parts by weight based on 100 parts by weight of the total of (a) and (b). Composition.
(c) 有機強化材、 無機強化材及び充填材からなる群から選ばれる 1種以上。 (c) at least one selected from the group consisting of organic reinforcements, inorganic reinforcements and fillers.
3. (a) と (b) とを、 (a) と (b) との合量中に (a) 7〜95重量%、 (b) 5〜3重量%の割合で含有する請求項 1または 2記載の樹脂組成物。3. Claim 1 wherein (a) and (b) are contained in the combined amount of (a) and (b) at a ratio of (a) 7 to 95% by weight and (b) 5 to 3% by weight. Or the resin composition according to 2.
4. フッ素樹脂のメルトインデックスが、 330°C、 5 k g荷重、 オリフィスの 径 2. 095mm, 長さ 8 m mの測定条件で測定し 0. 1以上である請求項 1、 2又は 3記載の樹脂組成物。 4. The resin according to claim 1, 2 or 3, wherein the fluorine resin has a melt index of at least 0.1 measured at 330 ° C, 5 kg load, orifice diameter 2.095 mm, length 8 mm. Composition.
5. フッ素樹脂がテトラフルォロエチレン Zペルフルォロ (アルキルビニルエー テル) 共重合体又はテトラフルォロエチレン/へキサフルォロプロピレン共重合 体である請求項 1〜4のいずれかに記載の樹脂組成物。  5. The method according to any one of claims 1 to 4, wherein the fluororesin is a tetrafluoroethylene Z perfluoro (alkyl vinyl ether) copolymer or a tetrafluoroethylene / hexafluoropropylene copolymer. Resin composition.
6. 下記 (a) と下記 (b 1 ) とを、 (a) と (b1 ) との合量中に (a) 70 〜95重量%、 (b 1 ) 5〜30重量%の割合で含有し、 さらに、 下記 (c) を 合量で、 (a) と (b 1 ) との合量 1 00重量部に対して 1 0〜250重量部の 割合で含有するする樹脂組成物。 6. the following (a) and the following (b 1), while the total amount of (a) and (b 1) (a) 70 ~95 wt%, (b 1) in a proportion of 5 to 30 wt% A resin composition containing the following (c) in a total amount of 10 to 250 parts by weight based on 100 parts by weight of the total of (a) and (b 1 ).
(a) ポリフエ二レンスルフィ ド。  (a) Polyphenylene sulfide.
(b 1 ) テトラフルォロエチレンノペルフルォロ (アルキルビュルエーテル) 共重合体又はテトラフルォロエチレン へキサフル才ロプロピレン共重合体。 (b 1 ) Tetrafluoroethylene noperfluoro (alkylbutyl ether) copolymer or tetrafluoroethylene hexafluoropropylene copolymer.
(c) 有機強化材、 無機強化材及び充填材からなる群から選ばれる 1種以上。 (c) at least one selected from the group consisting of organic reinforcements, inorganic reinforcements and fillers.
7. ポリフエ二レンスルフイ ドのメルトインデックスが、 330°C、 5 k g荷重 、 オリフィスの径 2. 095 mm, 長さ 8 m mの測定条件で測定し 0. 5〜50 0である請求項 1〜6のいずれかに記載の樹脂組成物。 7. The melt index of the polyphenylene sulfide is 0.5 to 500 when measured under the measurement conditions of 330 ° C, 5 kg load, orifice diameter 2.095 mm and length 8 mm. The resin composition according to any one of the above.
8. 請求項 1〜7のいずれかに記載の樹脂組成物を射出成形して得られる成形品 8. A molded product obtained by injection molding the resin composition according to any one of claims 1 to 7.
PCT/JP1999/001323 1998-03-19 1999-03-17 Resin composition WO1999047607A1 (en)

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US09/623,486 US6780944B1 (en) 1998-03-19 1999-03-17 Resin composition
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EP99909203A EP1065247B1 (en) 1998-03-19 1999-03-17 Resin composition

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US9243784B2 (en) 2012-12-20 2016-01-26 International Business Machines Corporation Semiconductor photonic package
US9400356B2 (en) 2013-03-14 2016-07-26 International Business Machines Corporation Fiber pigtail with integrated lid
US8923665B2 (en) 2013-03-15 2014-12-30 International Business Machines Corporation Material structures for front-end of the line integration of optical polarization splitters and rotators
US9360635B2 (en) 2014-07-09 2016-06-07 International Business Machines Corporation Dual-polymer fiber optic interface with melt-bond adhesive
JP6405787B2 (en) * 2014-08-18 2018-10-17 株式会社デンソー Rotor structure for liquid pump
US20200055234A1 (en) * 2016-10-21 2020-02-20 Toray Industries, Inc. Polyarylene sulfide resin powder granular article mixture and method for producing three-dimensional molded article
US20210206970A1 (en) 2018-05-25 2021-07-08 Daikin Industries, Ltd. Resin composition

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US6780944B1 (en) 2004-08-24
DE69938340T2 (en) 2009-03-26
DE69938340D1 (en) 2008-04-24
EP1065247A1 (en) 2001-01-03
JP4223089B2 (en) 2009-02-12
EP1065247A4 (en) 2001-07-04
EP1065247B1 (en) 2008-03-12
JPH11269383A (en) 1999-10-05

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